NL7300127A - - Google Patents

Info

Publication number
NL7300127A
NL7300127A NL7300127A NL7300127A NL7300127A NL 7300127 A NL7300127 A NL 7300127A NL 7300127 A NL7300127 A NL 7300127A NL 7300127 A NL7300127 A NL 7300127A NL 7300127 A NL7300127 A NL 7300127A
Authority
NL
Netherlands
Application number
NL7300127A
Other versions
NL173885C (en
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed filed Critical
Publication of NL7300127A publication Critical patent/NL7300127A/xx
Application granted granted Critical
Publication of NL173885C publication Critical patent/NL173885C/en

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J8/00Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
    • B01J8/02Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds
    • B01J8/06Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds in tube reactors; the solid particles being arranged in tubes
    • B01J8/067Heating or cooling the reactor
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28FDETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F27/00Control arrangements or safety devices specially adapted for heat-exchange or heat-transfer apparatus
    • F28F27/02Control arrangements or safety devices specially adapted for heat-exchange or heat-transfer apparatus for controlling the distribution of heat-exchange media between different channels
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28FDETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F9/00Casings; Header boxes; Auxiliary supports for elements; Auxiliary members within casings
    • F28F9/22Arrangements for directing heat-exchange media into successive compartments, e.g. arrangements of guide plates
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2208/00Processes carried out in the presence of solid particles; Reactors therefor
    • B01J2208/00008Controlling the process
    • B01J2208/00017Controlling the temperature
    • B01J2208/00106Controlling the temperature by indirect heat exchange
    • B01J2208/00168Controlling the temperature by indirect heat exchange with heat exchange elements outside the bed of solid particles
    • B01J2208/00212Plates; Jackets; Cylinders
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2208/00Processes carried out in the presence of solid particles; Reactors therefor
    • B01J2208/00008Controlling the process
    • B01J2208/00017Controlling the temperature
    • B01J2208/00106Controlling the temperature by indirect heat exchange
    • B01J2208/00168Controlling the temperature by indirect heat exchange with heat exchange elements outside the bed of solid particles
    • B01J2208/00212Plates; Jackets; Cylinders
    • B01J2208/00221Plates; Jackets; Cylinders comprising baffles for guiding the flow of the heat exchange medium
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2208/00Processes carried out in the presence of solid particles; Reactors therefor
    • B01J2208/00008Controlling the process
    • B01J2208/00017Controlling the temperature
    • B01J2208/00106Controlling the temperature by indirect heat exchange
    • B01J2208/00168Controlling the temperature by indirect heat exchange with heat exchange elements outside the bed of solid particles
    • B01J2208/00256Controlling the temperature by indirect heat exchange with heat exchange elements outside the bed of solid particles in a heat exchanger for the heat exchange medium separate from the reactor
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2208/00Processes carried out in the presence of solid particles; Reactors therefor
    • B01J2208/02Processes carried out in the presence of solid particles; Reactors therefor with stationary particles
    • B01J2208/023Details
    • B01J2208/024Particulate material
    • B01J2208/025Two or more types of catalyst
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2219/00Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J2219/00761Details of the reactor
    • B01J2219/00763Baffles
    • B01J2219/00765Baffles attached to the reactor wall
    • B01J2219/00777Baffles attached to the reactor wall horizontal
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28FDETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F9/00Casings; Header boxes; Auxiliary supports for elements; Auxiliary members within casings
    • F28F9/22Arrangements for directing heat-exchange media into successive compartments, e.g. arrangements of guide plates
    • F28F2009/222Particular guide plates, baffles or deflectors, e.g. having particular orientation relative to an elongated casing or conduit
    • F28F2009/226Transversal partitions

Landscapes

  • Engineering & Computer Science (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Devices And Processes Conducted In The Presence Of Fluids And Solid Particles (AREA)
  • Physical Or Chemical Processes And Apparatus (AREA)
  • Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
NLAANVRAGE7300127,A 1972-01-13 1973-01-04 REACTOR FOR PERFORMING EXOTHERMAL AND ENDOTHERMAL CHEMICAL REACTIONS. NL173885C (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
DE2201528A DE2201528C2 (en) 1972-01-13 1972-01-13 Reaction apparatus for carrying out exothermic and endothermic catalytic processes with radial flow of the heat exchange medium

Publications (2)

Publication Number Publication Date
NL7300127A true NL7300127A (en) 1973-07-17
NL173885C NL173885C (en) 1984-03-16

Family

ID=5832921

Family Applications (1)

Application Number Title Priority Date Filing Date
NLAANVRAGE7300127,A NL173885C (en) 1972-01-13 1973-01-04 REACTOR FOR PERFORMING EXOTHERMAL AND ENDOTHERMAL CHEMICAL REACTIONS.

Country Status (8)

Country Link
US (1) US3871445A (en)
JP (1) JPS5215272B2 (en)
BE (1) BE793928A (en)
DE (1) DE2201528C2 (en)
FR (1) FR2168092B1 (en)
GB (1) GB1415791A (en)
IT (1) IT972669B (en)
NL (1) NL173885C (en)

Families Citing this family (89)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DD103391A5 (en) * 1972-03-07 1974-01-20
DE2343788C3 (en) * 1973-08-30 1980-07-10 Wacker-Chemie Gmbh, 8000 Muenchen Device for the continuous implementation of chemical reactions, in particular polymerizations and processes for the continuous suspension polymerization of vinyl chloride
AU529228B2 (en) * 1977-07-13 1983-06-02 Nippon Shokubai Kagaku Kogyo Co. Ltd. Catalytic vapour phase oxidation
DE2903582B1 (en) * 1979-01-31 1980-11-20 Basf Ag, 6700 Ludwigshafen Tube bundle reactor for carrying out catalytic reactions in the gas phase
DE3034208A1 (en) * 1980-09-11 1982-04-22 GHT Gesellschaft für Hochtemperaturreaktor-Technik mbH, 5060 Bergisch Gladbach CANOPY WITH CATALYST MOLDED BODIES
US4635707A (en) * 1982-07-06 1987-01-13 Phillips Petroleum Company Method for varying shell fluid flow in shell and tube heat exchanger
DE3409159A1 (en) * 1984-03-13 1985-09-26 Deggendorfer Werft Und Eisenbau Gmbh, 8360 Deggendorf TUBE BUNCH REACTION APPARATUS
JPH03502422A (en) * 1988-12-13 1991-06-06 デークゲンドルファー・ヴェルフト・ウント・アイゼンバウ・ゲゼルシャフト・ミット・ベシュレンクター・ハフツング bundle tubular reactor
FR2655876B1 (en) * 1989-12-19 1994-03-11 Pecquet Tesson Ste Indle REACTOR FOR CATALYST CHEMICAL REACTIONS.
DE4013051A1 (en) * 1990-04-24 1991-11-07 Basf Ag METHOD FOR PRODUCING PHTHALIC ACID ANHYDRIDE FROM O-XYLOL
US5248483A (en) * 1991-03-28 1993-09-28 Phillips Petroleum Company Apparatus and methods for producing ceramic products
DE4123243A1 (en) * 1991-07-13 1993-01-14 Degussa TEMPERATURE VARIABLE TUBE BUNDLE HEAT EXCHANGER FOR CONSTANT QUANTITY RATIO OF EXCHANGE GAS AND HEAT EXCHANGE PROCESS
US5203405A (en) * 1992-02-03 1993-04-20 Phillips Petroleum Company Two pass shell and tube heat exchanger with return annular distributor
US5425415A (en) * 1993-06-15 1995-06-20 Abb Lummus Crest Inc. Vertical heat exchanger
DE4428017A1 (en) * 1994-08-08 1996-02-15 Bayer Ag Process for the preparation of aromatic amines
DE4428018A1 (en) * 1994-08-08 1996-02-15 Bayer Ag Process for the preparation of aromatic amines
US5544700A (en) * 1994-08-22 1996-08-13 General Electric Company Method and apparatus for preferential cooling
DE4431957A1 (en) * 1994-09-08 1995-03-16 Basf Ag Process for the catalytic gas-phase oxidation of propene to acrolein
DE4431949A1 (en) * 1994-09-08 1995-03-16 Basf Ag Process for the catalytic gas-phase oxidation of acrolein to acrylic acid
DE19542755A1 (en) 1995-11-16 1997-05-22 Basf Ag Multimetal oxides
GB9600350D0 (en) * 1996-01-09 1996-03-13 Ici Plc Heat exchange catalytic reactor
US5651386A (en) * 1996-03-14 1997-07-29 Nir; Ari Device for storing and discharging viscous liquid
DE19707943C2 (en) 1997-02-27 1999-07-08 Basf Ag Process for the preparation of phthalic anhydride and catalyst therefor
DE19836792A1 (en) * 1998-08-13 2000-02-17 Basf Ag Tube bundle reactor, for oxidation reactions, has partitioned headers allowing heat exchange medium supply to the lower header to be combined with co-current passage within the reactor
US6384274B1 (en) 1998-09-27 2002-05-07 Rohm And Haas Company Single reactor process for preparing acrylic acid from propylene having improved capacity
DE19851786A1 (en) 1998-11-10 2000-05-11 Basf Ag Multimetal oxide containing silver and vanadium oxide and its use
EP1080780B1 (en) * 1999-08-31 2007-08-01 Nippon Shokubai Co., Ltd. Reactor for catalytic gas phase oxidation
ZA200004211B (en) * 1999-08-31 2001-02-14 Nippon Catalytic Chem Ind Method for catalytic gas phase oxidation.
DE10011309A1 (en) * 2000-03-10 2001-09-13 Basf Ag Production of maleic anhydride comprises gas-phase oxidation of hydrocarbons in a reactor comprising at least two sequential cooled reaction zones at different temperatures
DE10024342A1 (en) 2000-05-17 2001-11-22 Basf Ag Reactor having a contact tube bundle, useful for oxidation reactions, has a heat exchange agent recycle loop fed through the chamber and rotating disks that rotate in the reactor center and edge.
CA2413388C (en) * 2000-06-29 2009-12-22 H2Gen Innovations Inc. Improved system for hydrogen generation through steam reforming of hydrocarbons and integrated chemical reactor for hydrogen production from hydrocarbons
DE10127365A1 (en) * 2001-06-06 2002-12-12 Basf Ag Pump, used for conveying heat transfer medium, comprises housing containing guide pipe and having opening in its lower part, via which heat transfer medium removed from lower region of reactor flows into housing
JP4017928B2 (en) * 2001-07-20 2007-12-05 ビーエーエスエフ アクチェンゲゼルシャフト Reactor, pump for use in the reactor, and method for performing oxidation reaction
US7316804B2 (en) * 2001-08-02 2008-01-08 Ineos Usa Llc Flow reactors for chemical conversions with heterogeneous catalysts
DE10144857A1 (en) * 2001-09-12 2003-03-27 Deggendorfer Werft Eisenbau Reactor arrangement used for the production of phthalic acid anhydride from o-xylol and/or naphthalene has a cooling stage and a secondary reactor located in the same housing as the main reactor
AU2003211899B2 (en) * 2002-03-11 2008-09-25 Mitsubishi Chemical Corporation Process for catalytic vapor phase oxidation
US8017816B2 (en) * 2002-04-22 2011-09-13 The Curators Of The University Of Missouri Method of producing lower alcohols from glycerol
US8252961B2 (en) 2002-04-22 2012-08-28 The Curators Of The University Of Missouri Method of producing lower alcohols from glycerol
US7663004B2 (en) * 2002-04-22 2010-02-16 The Curators Of The University Of Missouri Method of producing lower alcohols from glycerol
KR100450234B1 (en) * 2002-07-10 2004-09-24 주식회사 엘지화학 Catalytic oxidation reactor with enhanced heat exchanging system
DE10258180A1 (en) * 2002-12-12 2004-06-24 Basf Ag Preparation of chlorine involves oxidation of hydrogen chloride and gas stream comprising molecular oxygen in presence of fixed-bed catalyst is carried out in reactor having annular and disk-shaped deflection plates between catalyst tubes
DE10258153A1 (en) * 2002-12-12 2004-06-24 Basf Ag Preparation of chlorine by gas-phase oxidation of hydrogen chloride by a gas stream having molecular oxygen in presence of a fixed-bed catalyst is carried out in reactor having bundle of parallel catalyst tubes and deflector plate
EP1569745B1 (en) * 2002-12-12 2019-03-20 MAN Energy Solutions SE Shell-and-tube type reactor for catalytic gas phase reactions
DE10312788A1 (en) * 2003-03-21 2004-09-30 Behr Gmbh & Co. Kg Exhaust gas heat exchanger and sealing device for exhaust gas heat exchanger
DE10334132A1 (en) 2003-07-25 2005-04-07 Basf Ag Silver, vanadium and a promoter metal-containing multimetal and its use
BRPI0413440A (en) * 2003-08-14 2006-10-17 Basf Ag Process for the preparation of (meth) acrolein and / or (meth) acrylic acid by heterogeneously catalyzed partial gas phase oxidation
KR100553825B1 (en) * 2003-09-01 2006-02-21 주식회사 엘지화학 Method of producing unsaturated aldehyde and unsaturated acid in fixed-bed catalytic partial oxidation reactor with enhanced heat control system
TWI288127B (en) 2003-12-24 2007-10-11 Lg Chemical Ltd Method of producing unsaturated acid in fixed-bed catalytic partial oxidation reactor with enhanced heat control system
EP1748839B1 (en) 2004-05-07 2020-04-01 Basf Se Method for structurally filling contact tubes of a bank of contact tubes
KR101248672B1 (en) * 2004-09-15 2013-03-28 가부시끼가이샤 구레하 Apparatus and method for solid-liquid contact
JP4205035B2 (en) * 2004-09-27 2009-01-07 住友化学株式会社 Multi-tube reactor for catalytic gas phase reaction
KR100677051B1 (en) * 2005-03-18 2007-02-01 주식회사 엘지화학 Method of producing unsaturated acid from olefin
KR100838970B1 (en) * 2005-04-29 2008-06-16 주식회사 엘지화학 Annular-type distributor with improved flow uniformity
US20070135301A1 (en) * 2005-12-08 2007-06-14 Sud-Chemie Inc. Catalyst for the production of polyols by hydrogenolysis of carbohydrates
KR100898692B1 (en) * 2006-01-18 2009-05-22 주식회사 엘지화학 Reactor with improved heat transfer performance, method for producing oxide by using the reactor, and method for increasing parallel flow of heat transfer rate
KR100886083B1 (en) * 2006-01-31 2009-02-26 주식회사 엘지화학 Reactor with improved heat transfer performance, and method for producing oxide by using the reactor
WO2007083927A1 (en) * 2006-01-18 2007-07-26 Lg Chem, Ltd. Reactor with improved heat transfer performance
EP1734030A1 (en) 2006-01-18 2006-12-20 BASF Aktiengesellschaft Method for long term operation of a heterogeneously catalysed gas phase partial oxidation of an organic educt
KR100847199B1 (en) * 2006-01-31 2008-07-17 주식회사 엘지화학 Reactor with improved heat transfer performance, method for producing oxide by using the reactor, and method for increasing
DE102006007619A1 (en) * 2006-02-18 2007-08-23 Bayer Materialscience Ag Preparing aniline, useful to prepare e.g. di- and polyamine, comprises hydrogenating nitrobenzene to obtain raw aniline, extracting raw aniline with aqueous alkali metal hydroxide solution and separating aqueous- and organic phase
DE102006007620A1 (en) * 2006-02-18 2007-08-23 Bayer Materialscience Ag Production of crude aniline for use in producing di- and polyamines, involves purifying crude aniline by adding aqueous alkali metal hydroxide solution to crude aniline prior to and/or during distillation
TWI322882B (en) * 2006-02-24 2010-04-01 Lg Chemical Ltd Annular distributor having guide vane to improve flow rate distribution, reactor/heat exchanger including the annular distributor and method of producing unsaturated aldehyde or unsaturated acid from olefin by catalytic gas phase oxidation in the reactor
DE102006035203A1 (en) * 2006-07-29 2008-01-31 Bayer Materialscience Ag Process for the preparation of aromatic amines
DE102006052989A1 (en) * 2006-11-10 2008-05-15 Bayer Materialscience Ag Process for the removal of compounds with phenolic hydroxy groups from aromatic amines
DE102007010422A1 (en) 2007-03-01 2008-09-04 Basf Se Preparation of a catalyst, useful in the heterogeneously catalyzed partial gas phase oxidation of acrolein to acrylic acid, comprises attaching one of the active mass to the surface of the carrier body with the help of a binding agent
DE102007017080A1 (en) 2007-04-10 2008-10-16 Basf Se Method for feeding a longitudinal section of a contact tube
DE102007028332A1 (en) 2007-06-15 2008-12-18 Basf Se A method for feeding a reactor with a fixed catalyst bed comprising at least annular shaped catalyst bodies K.
DE102007039091A1 (en) 2007-08-18 2009-02-19 Bayer Materialscience Ag Process for the purification of aromatic amines
DE102007045125A1 (en) 2007-09-20 2009-04-02 Bayer Technology Services Gmbh Process for the preparation of aromatic amines
DE102007048441A1 (en) * 2007-10-10 2009-04-16 Bomat Heiztechnik Gmbh heat exchangers
DE102007061477A1 (en) 2007-12-20 2009-07-02 Man Dwe Gmbh Tube reactor
DE102009019436A1 (en) * 2009-04-29 2010-11-04 Bayer Materialscience Ag Process for the preparation of aromatic amines
DE102009025374A1 (en) 2009-06-18 2010-12-23 Bayer Materialscience Ag Process for the preparation of aromatic amines
DE102009047291A1 (en) 2009-11-30 2010-09-23 Basf Se Producing (meth)acrolein, by heterogeneous catalyzed gas phase-partial oxidation, comprises guiding reaction gas mixture through a fresh fixed catalyst bed present in a reactor at increased temperature
JP5104885B2 (en) * 2010-02-09 2012-12-19 三菱化学株式会社 Catalytic reactor
KR20130041145A (en) 2010-07-30 2013-04-24 바이엘 인텔렉쳐 프로퍼티 게엠베하 Method for continuously producing nitrobenzene
DE102010048405A1 (en) 2010-10-15 2011-05-19 Basf Se Long term operation of heterogeneously catalyzed partial gas phase oxidation of propene to acrolein, comprises conducting reaction gas input mixture containing propene, molecular oxygen and inert gas, through solid catalyst bed
EP2663544B1 (en) 2011-01-11 2014-12-24 Bayer Intellectual Property GmbH Process for preparing aromatic amines
DE102011076931A1 (en) 2011-06-03 2012-12-06 Basf Se Aqueous solution containing acrylic acid and its conjugate base
DE102011084476A1 (en) * 2011-10-13 2013-04-18 Man Diesel & Turbo Se Tube reactor
EP2653461A1 (en) 2012-04-16 2013-10-23 Bayer MaterialScience AG Method for improved stopping of the reaction when producing aromatic amines from nitroaromatics
EP2653462A1 (en) 2012-04-16 2013-10-23 Bayer MaterialScience AG Method for improved starting the reaction when producing aromatic amines from nitroaromatics
DE102012207811A1 (en) 2012-05-10 2012-07-12 Basf Se Heterogeneously catalyzed gas phase partial oxidation of (meth)acrolein to (meth)acrylic acid using a catalytically active multimetal oxide mass
DE102013218628A1 (en) 2013-09-17 2014-03-06 Basf Se Catalyst useful for producing alpha, beta-unsaturated carboxylic acid by gas phase oxidation of alpha, beta-unsaturated aldehyde, comprises support molded body with active material applied on support molded body
DE102014203725A1 (en) 2014-02-28 2015-09-03 Basf Se Oxidation catalyst with saddle-shaped carrier shaped body
DE102016002679A1 (en) 2016-03-04 2017-09-21 Hans-Jürgen Eberle Apparatus and method for carrying out heterogeneously catalyzed exothermic gas phase reactions
CN105890402B (en) * 2016-06-07 2018-01-30 纳盛洁净技术(苏州)有限公司 A kind of muitishell shell-and-tube heat exchanger
EP3360611B1 (en) * 2017-02-10 2021-04-28 Technobell D.O.O. Koper Improved double zone tubular reactor and method for carrying out maleic anhydride production by n-butane oxidation
EP3643699B1 (en) 2018-10-17 2021-09-22 Covestro Intellectual Property GmbH & Co. KG Method for the purification of aniline

Family Cites Families (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US688472A (en) * 1898-07-14 1901-12-10 Basf Ag Apparatus for the manufacture of sulfuric anhydrid.
US652119A (en) * 1898-07-14 1900-06-19 Basf Ag Method of making sulfuric anhydrid.
NL282221A (en) * 1961-08-23
US3147084A (en) * 1962-03-08 1964-09-01 Shell Oil Co Tubular catalytic reactor with cooler
US3353923A (en) * 1962-05-25 1967-11-21 Reichhold Chemicals Inc Catalytic reactor tube liner
US3532472A (en) * 1967-03-20 1970-10-06 Shell Oil Co Apparatus for carrying out partial oxidation of organic compounds
CH493811A (en) * 1967-09-06 1970-07-15 Basf Ag Heat exchange device
US3490521A (en) * 1968-03-12 1970-01-20 Westinghouse Electric Corp Tube and shell heat exchanger
US3595308A (en) * 1969-08-01 1971-07-27 Lewis H Durbin Apparatus for cooling liquids
US3623549A (en) * 1970-08-14 1971-11-30 Smitherm Industries Heat exchange methods and apparatus
DE2062095C3 (en) * 1970-12-17 1974-04-04 Deggendorfer Werft Und Eisenbau Gmbh, 8360 Deggendorf Reaction apparatus for carrying out exothermic chemical reactions

Also Published As

Publication number Publication date
FR2168092A1 (en) 1973-08-24
GB1415791A (en) 1975-11-26
JPS4880473A (en) 1973-10-27
BE793928A (en) 1973-05-02
US3871445A (en) 1975-03-18
IT972669B (en) 1974-05-31
NL173885C (en) 1984-03-16
DE2201528B1 (en) 1972-11-02
FR2168092B1 (en) 1977-07-29
JPS5215272B2 (en) 1977-04-27
DE2201528C2 (en) 1974-12-12

Similar Documents

Publication Publication Date Title
FR2168092B1 (en)
FR2175145A1 (en)
FR2175146B3 (en)
JPS4879238A (en)
FR2202250B1 (en)
JPS4984454A (en)
HU166517B (en)
JPS495949A (en)
JPS491525U (en)
JPS5222179Y2 (en)
JPS4914994U (en)
FI47058B (en)
JPS4940984U (en)
CH582683A5 (en)
BG18378A1 (en)
CH565475A5 (en)
CH578671A5 (en)
CH578563A5 (en)
CH1765473A4 (en)
CH578307A5 (en)
CH577744A5 (en)
CH576928A5 (en)
CH576683A5 (en)
CH576435A5 (en)
CH576369A5 (en)

Legal Events

Date Code Title Description
BA A request for search or an international-type search has been filed
BB A search report has been drawn up
BC A request for examination has been filed
V1 Lapsed because of non-payment of the annual fee